Mixture of Diethyl malonate + Methyl Alcohol

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Diethyl malonate

Name
Diethyl malonate
InChI
InChI=1S/C7H12O4/c1-3-10-6(8)5-7(9)11-4-2/h3-5H2,1-2H3
InChI Key
IYXGSMUGOJNHAZ-UHFFFAOYSA-N
Formula
C7H12O4
SMILES
CCOC(=O)CC(=O)OCC
Mol. Weight (g/mol)
160.17
CAS
105-53-3

Methyl Alcohol

Name
Methyl Alcohol
InChI
InChI=1S/CH4O/c1-2/h2H,1H3
InChI Key
OKKJLVBELUTLKV-UHFFFAOYSA-N
Formula
CH4O
SMILES
CO
Mol. Weight (g/mol)
32.04
CAS
67-56-1
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ρl - Mass density, kg/m3 (2)

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
288.20 0.0500 0.2760
288.20 0.0996 0.5130
288.20 0.1496 0.6980
288.20 0.2011 0.8580
288.20 0.2515 0.9890
288.20 0.3009 1.093
288.20 0.3506 1.175
288.20 0.3988 1.25
288.20 0.4486 1.295
288.20 0.4993 1.311
288.20 0.5500 1.319
288.20 0.5995 1.285
288.20 0.6464 1.256
288.20 0.6980 1.18
288.20 0.7453 1.093
288.20 0.7969 0.9780
288.20 0.8536 0.7960
288.20 0.9030 0.5820
288.20 0.9500 0.3350
298.20 0.0500 0.3070
298.20 0.0996 0.5550
298.20 0.1496 0.7630
298.20 0.2011 0.9370
298.20 0.2515 1.083
298.20 0.3009 1.198
298.20 0.3506 1.286
298.20 0.3988 1.361
298.20 0.4486 1.402
298.20 0.4993 1.426
298.20 0.5500 1.435
298.20 0.5995 1.408
298.20 0.6464 1.352
298.20 0.6980 1.272
298.20 0.7453 1.184
298.20 0.7969 1.016
298.20 0.8536 0.7680
298.20 0.9030 0.5860
298.20 0.9500 0.3230
313.20 0.0500 0.3390
313.20 0.0996 0.6100
313.20 0.1496 0.8510
313.20 0.2011 1.042
313.20 0.2515 1.198
313.20 0.3009 1.33
313.20 0.3506 1.434
313.20 0.3988 1.509
313.20 0.4486 1.563
313.20 0.4993 1.58
313.20 0.5500 1.575
313.20 0.5995 1.543
313.20 0.6464 1.486
313.20 0.6980 1.387
313.20 0.7453 1.268
313.20 0.7969 1.086
313.20 0.8536 0.8440
313.20 0.9030 0.6020
313.20 0.9500 0.3010
328.20 0.0500 0.3650
328.20 0.0996 0.6730
328.20 0.1496 0.9260
328.20 0.2011 1.146
328.20 0.2515 1.324
328.20 0.3009 1.459
328.20 0.3506 1.572
328.20 0.3988 1.647
328.20 0.4486 1.703
328.20 0.4993 1.709
328.20 0.5500 1.713
328.20 0.5995 1.657
328.20 0.6464 1.591
328.20 0.6980 1.475
328.20 0.7453 1.321
328.20 0.7969 1.163
328.20 0.8536 0.8930
328.20 0.9030 0.6070
328.20 0.9500 0.1980

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
288.20 0.0500 0.2760
288.20 0.0996 0.5130
288.20 0.1496 0.6980
288.20 0.2011 0.8580
288.20 0.2515 0.9890
288.20 0.3009 1.093
288.20 0.3506 1.175
288.20 0.3988 1.25
288.20 0.4486 1.295
288.20 0.4993 1.311
288.20 0.5500 1.319
288.20 0.5995 1.285
288.20 0.6464 1.256
288.20 0.6980 1.18
288.20 0.7453 1.093
288.20 0.7969 0.9780
288.20 0.8536 0.7960
288.20 0.9030 0.5820
288.20 0.9500 0.3350
298.20 0.0500 0.3070
298.20 0.0996 0.5550
298.20 0.1496 0.7630
298.20 0.2011 0.9370
298.20 0.2515 1.083
298.20 0.3009 1.198
298.20 0.3506 1.286
298.20 0.3988 1.361
298.20 0.4486 1.402
298.20 0.4993 1.426
298.20 0.5500 1.435
298.20 0.5995 1.408
298.20 0.6464 1.352
298.20 0.6980 1.272
298.20 0.7453 1.184
298.20 0.7969 1.016
298.20 0.8536 0.7680
298.20 0.9030 0.5860
298.20 0.9500 0.3230
313.20 0.0500 0.3390
313.20 0.0996 0.6100
313.20 0.1496 0.8510
313.20 0.2011 1.042
313.20 0.2515 1.198
313.20 0.3009 1.33
313.20 0.3506 1.434
313.20 0.3988 1.509
313.20 0.4486 1.563
313.20 0.4993 1.58
313.20 0.5500 1.575
313.20 0.5995 1.543
313.20 0.6464 1.486
313.20 0.6980 1.387
313.20 0.7453 1.268
313.20 0.7969 1.086
313.20 0.8536 0.8440
313.20 0.9030 0.6020
313.20 0.9500 0.3010
328.20 0.0500 0.3650
328.20 0.0996 0.6730
328.20 0.1496 0.9260
328.20 0.2011 1.146
328.20 0.2515 1.324
328.20 0.3009 1.459
328.20 0.3506 1.572
328.20 0.3988 1.647
328.20 0.4486 1.703
328.20 0.4993 1.709
328.20 0.5500 1.713
328.20 0.5995 1.657
328.20 0.6464 1.591
328.20 0.6980 1.475
328.20 0.7453 1.321
328.20 0.7969 1.163
328.20 0.8536 0.8930
328.20 0.9030 0.6070
328.20 0.9500 0.1980

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 796.406
288.15 0.0500 841.286
288.15 0.1000 876.23
288.15 0.1501 904.185
288.15 0.2001 926.962
288.15 0.2501 945.901
288.15 0.3001 961.96
288.15 0.3500 975.573
288.15 0.4001 987.417
288.15 0.4503 997.752
288.15 0.5004 1006.896
288.15 0.5497 1014.881
288.15 0.6000 1022.041
288.15 0.6495 1028.476
288.15 0.6997 1034.33
288.15 0.7978 1044.36
288.15 0.9009 1053.152
288.15 1.0000 1060.326
298.15 0.0000 786.987
298.15 0.0500 831.536
298.15 0.1000 866.252
298.15 0.1501 894.037
298.15 0.2001 916.671
298.15 0.2501 935.504
298.15 0.3001 951.502
298.15 0.3500 965.04
298.15 0.4001 976.822
298.15 0.4503 987.12
298.15 0.5004 996.235
298.15 0.5497 1004.184
298.15 0.6000 1011.322
298.15 0.6495 1017.743
298.15 0.6997 1023.585
298.15 0.7978 1033.607
298.15 0.9009 1042.395
298.15 1.0000 1049.603
313.15 0.0000 772.74
313.15 0.0500 816.754
313.15 0.1000 851.13
313.15 0.1501 878.631
313.15 0.2001 901.091
313.15 0.2501 919.763
313.15 0.3001 935.636
313.15 0.3500 949.084
313.15 0.4001 960.784
313.15 0.4503 971.04
313.15 0.5004 980.1
313.15 0.5497 988.016
313.15 0.6000 995.132
313.15 0.6495 1001.516
313.15 0.6997 1007.366
313.15 0.7978 1017.382
313.15 0.9009 1026.218
313.15 1.0000 1033.498
328.15 0.0000 758.201
328.15 0.0500 801.691
328.15 0.1000 835.697
328.15 0.1501 862.956
328.15 0.2001 885.223
328.15 0.2501 903.75
328.15 0.3001 919.517
328.15 0.3500 932.879
328.15 0.4001 944.523
328.15 0.4503 954.725
328.15 0.5004 963.763
328.15 0.5497 971.649
328.15 0.6000 978.761
328.15 0.6495 985.159
328.15 0.6997 991.006
328.15 0.7978 1001.066
328.15 0.9009 1009.978
328.15 1.0000 1017.336

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl malonate (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0000 796.406
288.15 0.0500 841.286
288.15 0.1000 876.23
288.15 0.1501 904.185
288.15 0.2001 926.962
288.15 0.2501 945.901
288.15 0.3001 961.96
288.15 0.3500 975.573
288.15 0.4001 987.417
288.15 0.4503 997.752
288.15 0.5004 1006.896
288.15 0.5497 1014.881
288.15 0.6000 1022.041
288.15 0.6495 1028.476
288.15 0.6997 1034.33
288.15 0.7978 1044.36
288.15 0.9009 1053.152
288.15 1.0000 1060.326
298.15 0.0000 786.987
298.15 0.0500 831.536
298.15 0.1000 866.252
298.15 0.1501 894.037
298.15 0.2001 916.671
298.15 0.2501 935.504
298.15 0.3001 951.502
298.15 0.3500 965.04
298.15 0.4001 976.822
298.15 0.4503 987.12
298.15 0.5004 996.235
298.15 0.5497 1004.184
298.15 0.6000 1011.322
298.15 0.6495 1017.743
298.15 0.6997 1023.585
298.15 0.7978 1033.607
298.15 0.9009 1042.395
298.15 1.0000 1049.603
313.15 0.0000 772.74
313.15 0.0500 816.754
313.15 0.1000 851.13
313.15 0.1501 878.631
313.15 0.2001 901.091
313.15 0.2501 919.763
313.15 0.3001 935.636
313.15 0.3500 949.084
313.15 0.4001 960.784
313.15 0.4503 971.04
313.15 0.5004 980.1
313.15 0.5497 988.016
313.15 0.6000 995.132
313.15 0.6495 1001.516
313.15 0.6997 1007.366
313.15 0.7978 1017.382
313.15 0.9009 1026.218
313.15 1.0000 1033.498
328.15 0.0000 758.201
328.15 0.0500 801.691
328.15 0.1000 835.697
328.15 0.1501 862.956
328.15 0.2001 885.223
328.15 0.2501 903.75
328.15 0.3001 919.517
328.15 0.3500 932.879
328.15 0.4001 944.523
328.15 0.4503 954.725
328.15 0.5004 963.763
328.15 0.5497 971.649
328.15 0.6000 978.761
328.15 0.6495 985.159
328.15 0.6997 991.006
328.15 0.7978 1001.066
328.15 0.9009 1009.978
328.15 1.0000 1017.336

Sources